EP2145681A1 - Methode pour la reduction du poid moleculaire de caoutschouc nitrile - Google Patents

Methode pour la reduction du poid moleculaire de caoutschouc nitrile Download PDF

Info

Publication number
EP2145681A1
EP2145681A1 EP09164639A EP09164639A EP2145681A1 EP 2145681 A1 EP2145681 A1 EP 2145681A1 EP 09164639 A EP09164639 A EP 09164639A EP 09164639 A EP09164639 A EP 09164639A EP 2145681 A1 EP2145681 A1 EP 2145681A1
Authority
EP
European Patent Office
Prior art keywords
alkyl
catalyst
general formula
aryl
alkoxy
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP09164639A
Other languages
German (de)
English (en)
Other versions
EP2145681B1 (fr
Inventor
Julia Maria Müller
Oskar Nuyken
Werner Obrecht
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Lanxess Deutschland GmbH
Original Assignee
Lanxess Deutschland GmbH
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Lanxess Deutschland GmbH filed Critical Lanxess Deutschland GmbH
Priority to EP09164639A priority Critical patent/EP2145681B1/fr
Publication of EP2145681A1 publication Critical patent/EP2145681A1/fr
Application granted granted Critical
Publication of EP2145681B1 publication Critical patent/EP2145681B1/fr
Not-in-force legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/22Organic complexes
    • B01J31/2265Carbenes or carbynes, i.e.(image)
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/22Organic complexes
    • B01J31/2265Carbenes or carbynes, i.e.(image)
    • B01J31/2269Heterocyclic carbenes
    • B01J31/2273Heterocyclic carbenes with only nitrogen as heteroatomic ring members, e.g. 1,3-diarylimidazoline-2-ylidenes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/22Organic complexes
    • B01J31/2265Carbenes or carbynes, i.e.(image)
    • B01J31/2278Complexes comprising two carbene ligands differing from each other, e.g. Grubbs second generation catalysts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2231/00Catalytic reactions performed with catalysts classified in B01J31/00
    • B01J2231/50Redistribution or isomerisation reactions of C-C, C=C or C-C triple bonds
    • B01J2231/54Metathesis reactions, e.g. olefin metathesis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2531/00Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/80Complexes comprising metals of Group VIII as the central metal
    • B01J2531/82Metals of the platinum group
    • B01J2531/821Ruthenium

Definitions

  • the present invention relates to catalyst systems, their use for catalyzing metathesis reactions, and more particularly to a process for molecular weight reduction of nitrile rubber by metathesis using these catalyst systems.
  • Metathesis reactions are widely used in chemical syntheses, such as ring-closing metathesis (RCM), cross-metathesis (CM), ring-opening metathesis (ROM), ring-opening metathesis polymerization (ROMP), cyclic diene metathesis polymerizations (ADMET), self-metathesis, alkenes with alkynes (enyne reactions), polymerization of alkynes and olefination of carbonyls ( WO-A-97/06185 and Platinum Metals Rev., 2005, 49 (3), 123-137 ). Metathesis reactions are used, for example, for the olefin synthesis, for the ring-opening polymerization of norbornene derivatives, for the depolymerization of unsaturated polymers and for the synthesis of telechelics.
  • RCM ring-closing metathesis
  • CM cross-metathesis
  • ROM ring-opening metathesis
  • ROMP ring-opening metathesis polymerization
  • Metathesis catalysts are among others from the WO-A-96/04289 and WO-A-97/06185 known. They have the following basic structure: where M is osmium or ruthenium, R is the same or different organic radicals of great structural variation, X 1 and X 2 are anionic ligands, and L is neutral electron donors.
  • anionic ligands in the literature for such metathesis catalysts is always understood to mean those ligands which, when considered as remote from the metal center, are negatively charged when the electron shell is closed.
  • Nitrile rubber also abbreviated to "NBR” is understood to mean rubbers which are copolymers or terpolymers of at least one ⁇ , ⁇ -unsaturated nitrile, at least one conjugated diene and optionally one or more further copolymerizable monomers.
  • the degree of hydrogenation of the copolymerized diene units is usually in a range of 50 to 100%.
  • Hydrogenated nitrile rubber is a special rubber that has very good heat resistance, excellent resistance to ozone and chemicals, and excellent oil resistance.
  • HNBR has found wide use in a variety of applications.
  • HNBR is used, for example, for seals, hoses, belts and damping elements in the automotive sector, as well as for stators, borehole seals and valve seals in the field of oil production as well as for numerous parts of the aerospace industry, the electrical industry, mechanical engineering and shipbuilding.
  • HNBR types typically have a Mooney viscosity (ML 1 + 4 at 100 ° C) in the range of 55 to 120, which is a number average molecular weight M n (determination method: gel permeation chromatography (GPC) versus polystyrene equivalents) Range of approximately 200,000 to 700,000.
  • M n determination method: gel permeation chromatography (GPC) versus polystyrene equivalents
  • the residual double bond content is usually in a range of 0 to 18% (determined by NMR or IR spectroscopy). Of so-called "fully hydrogenated types" is already spoken in the art, if the residual double bond content is a maximum of about 0.9%.
  • HNBR types having the above-mentioned relatively high Mooney viscosities are subject to limitations.
  • HNBR types are desirable which have a lower molecular weight and thus a lower Mooney viscosity, as this significantly improves the processability.
  • thermomechanical treatment z. B. on a rolling mill or in a screw unit ( EP-A-0 419 952 ) possible.
  • this thermomechanical degradation has the disadvantage that by partial oxidation functional groups such as hydroxyl, keto, carboxylic acid and ester groups are incorporated into the molecule and, in addition, the microstructure of the polymer is substantially altered.
  • the lowest Mooney viscosity of an NBR feedstock that can be processed without difficulty in an established large-scale plant is about 30 Mooney units (ML 1 + 4 at 100 ° C).
  • the Mooney viscosity of the hydrogenated nitrile rubber obtained with such NBR feedstock is on the order of 55 Mooney units (ML 1 + 4 at 100 ° C).
  • the Mooney viscosity is determined according to ASTM standard D 1646.
  • this problem is solved by controlling the molecular weight of the nitrile rubber before hydrogenation by degradation to a Mooney viscosity (ML 1 + 4 at 100 ° C) of less than 30 Mooney units or a number average molecular weight of M n ⁇ 70,000 g / mol reduced.
  • the reduction of the molecular weight can be achieved by metathesis, in which one usually adds low molecular weight 1-olefins. Described is the metathesis of nitrile rubber, for example in WO-A-02/100905 .
  • the metathesis reaction is expediently carried out in the same solvent as the hydrogenation reaction, so that the degraded nitrile rubber does not have to be isolated from the solvent after the decomposition reaction has ended, before it is subjected to the subsequent hydrogenation.
  • Metathesis catalysts which are tolerant of polar groups, particularly nitrile groups, are used to catalyze the metathesis degradation reaction.
  • WO-A-02/100905 and the WO-A-02/100941 there is described a process comprising the degradation of nitrile rubber starting polymers by olefin metathesis followed by hydrogenation to low Mooney viscosity HNBR.
  • a nitrile rubber is reacted in a first step in the presence of a co-olefin and special complex catalysts based on osmium, ruthenium, molybdenum or tungsten and hydrogenated in a second step.
  • Hydrogenated nitrile rubbers having a weight average molecular weight (M w ) in the range of 30,000 to 250,000, a Mooney viscosity (ML 1 + 4 at 100 ° C.) in the range from 3 to 50 and a polydispersity index PDI of less than 2.5 are obtainable in this way ,
  • nitrile rubber For the metathesis of nitrile rubber, it is possible, for example, to use the catalyst bis (tricyclohexylphosphine) benzylidene ruthenium dichloride shown below. After metathesis and hydrogenation, the nitrile rubbers have a lower molecular weight and a narrower molecular weight distribution than the prior art hydrogenated nitrile rubbers that can be produced hitherto.
  • EP-A-1 825 913 new catalyst systems for metathesis are described in which one or more salts are used in addition to the actual metathesis catalyst.
  • This combination of one or more salts with the metathesis catalyst leads to an increase in the activity of the catalyst, a synergistic effect.
  • For the anions and cations of these salts a variety of meanings is possible in each case, which can be selected from various lists. Be particularly advantageous proves in the examples of EP-A-1 825 913 for the metathesis degradation of rubbers, such as nitrile rubbers, as well as for the ring-closing metathesis of diethyl diallylmalonate the use of lithium bromide.
  • catalysts are those which coordinate with the metal center of a ruthenium or osmium carbene via an oxygen-, nitrogen- or sulfur-containing substituent.
  • the Grubbs (II) catalyst, the Hoveyda, the Buchmeiser Nuyken and the Grela catalyst are used.
  • the object of the present invention was to provide novel catalyst systems which can be used universally in various types of metathesis reactions, lead to increases in activity on the basis of various metathesis catalysts and thus allow a reduction in the amount of catalyst and thus in particular the amount of precious metals contained therein. Especially for the metathetic degradation of nitrile rubber possibilities should be found that allow an increase in activity of the catalyst used without gelling of the nitrile rubber.
  • metathesis catalysts can be significantly increased when used in combination with fluorine-containing boron compounds.
  • molecular weight degradation of nitrile rubber by metathesis can be significantly improved if the metathesis catalyst is used as a system in combination with fluorine-containing boron compounds.
  • This combination increases the reaction rate of metathesis reactions and, in particular in NBR metathesis, significantly narrower molecular weight distributions and lower molecular weights can be obtained without gelling.
  • the amount of metathesis catalyst can be reduced by the addition of fluorine-containing boron compounds.
  • compounds of the general formula (Z) in which X is chlorine, bromine or a group -OR or -NR 2 , where R independently of one another in each case represent straight-chain or branched C 1 -C 30, are used in the catalyst system -Alkyl, preferably C 1 -C 20 -alkyl, more preferably C 1 -C 12 -alkyl, C 3 -C 20 -cycloalkyl, preferably C 3 -C 10 -cycloalkyl, more preferably C 5 -C 8 -cycloalkyl, C C 2 -C 20 -alkenyl, preferably C 2 -C 18 -alkenyl, C 2 -C 20 -alkynyl-, preferably C 2 -C 18 -alkynyl, C 6 -C 24 -aryl, preferably C 6 -C 14 -aryl, C 4 -C 23 -heteroaryl, where these heteroaryl
  • compounds of the general formula (Z) are used in the catalyst system in which R in the context of the radicals OR and NR 2 are each methyl, ethyl, n-propyl, isopropyl, n-butyl, Butyl, tert-butyl, n-pentyl, i-pentyl, tert-pentyl, hexyl, decyl, dodecyl, oleyl, phenyl or sterically hindered phenyl.
  • the part BF m X n is preferably BF 3 , BF 2 Cl, BFCl 2 BF 2 Br, BFBr 2 , BF 2 (OC 2 H 5 ), BF (OC 2 H 5 ) 2 , BF 2 (CH 3 ) and BF (CH 3 ) 2 .
  • BF m X n is particularly preferably BF 3 .
  • the radicals R independently of one another preferably denote hydrogen, straight-chain or branched C 1 -C 30 -alkyl, particularly preferably straight-chain or branched C 1 -C 12 -alkyl, C 3 -C 20 -cycloalkyl, particularly preferably C 5 -C 8 -cycloalkyl , straight-chain or branched C 2 -C 20 -alkenyl, particularly preferably straight-chain or branched C 2 -C 14 -alkenyl, straight-chain or branched C 2 -C 20 -alkynyl, particularly preferably straight-chain or branched C 2 -C 14 -alkynyl, C 6 -C 24 -aryl, more preferably C 6 -C 14 aryl is, where all the abovementioned radicals may each optional, preferably fluorine or chlorine, alkoxy, aryl or heteroaryl radicals substituted by one or more alkyl, halogen could be.
  • two radicals R may also be bridged to form a cyclic group which incorporates the common atom (s) to which they are attached may be aliphatic or aromatic in nature, optionally substituted, and may additionally contain one or more heteroatoms, preferably oxygen or nitrogen.
  • Examples of compounds D of the general formula (2) are: water, dimethyl ether, diethyl ether, di-n-propyl ether, di-i-propyl ether, di-n-butyl ether, di-i-butyl ether, di-t-butyl ether, methyl t-butyl ether, dimethoxyethane, di-n-butoxyethane, diphenyl ether, methyl phenyl ether, ethyl phenyl ether, tetrahydrofuran, tetrahydropyran. Preference is given to water, diethyl ether, tetrahydrofuran and tetrahydropyran.
  • Examples of compounds D of the general formula (3) are: methanol, ethanol, n-propanol, i-propanol, n-butanol, t-butanol, phenol, pyrocatechol, anisole and salicylic acid.
  • Examples of compounds D of the general formula (4) are: formic acid, acetic acid, propionic acid, citric acid, trichloroacetic acid, trifluoroacetic acid and benzoic acid.
  • Examples of compounds D of the general formula (5) are: hydrogen sulfide, methylmercaptan, n-hexylmercaptan, t-butylmercaptan, t-nonylmercaptan, n-dodecylmercaptan and t-dodecylmercaptan, dimethylsulfide, diethylsulfide, diisopropylsulfide, tetrahydrothiophene and diphenylsulfide.
  • Examples of compounds D of the general formula (6) are dimethylsulfoxide, diethylsulfoxide, diisopropylsulfoxide, butylmethylsulfoxide and tetrahydrothiophene-1-oxide.
  • Examples of compounds D of the general formula (7) are dimethylsulfone, diethylsulfone, diisopropylsulfone, butylmethylsulfone and sulfolane (tetrahydrothiophene-1,1-dioxide).
  • Examples of compounds D of the general formula (8a, 8b and 8c) are: trimethylamine, triethylamine, triethanolamine, aniline, methylaniline, dimethylaniline, pyridine, pyrimidine, pyrol, pyrolidine, tetramethylethylenediamine, tetraethylethylenediamine, ammonia, methylamine, ethylamine, propylamine, diethylamine and dimethylamine.
  • Examples of compounds D of the general formula (9a) are: phosphine, trimethylphosphine, triethylphosphine, triisopropylphosphine, tricyclohexylphosphine, triphenylphosphine and tris (phenylsulfonic acid ) phosphine and its salts.
  • An example of a compound D of the general formula (9b) is tetraphenyldiphosphine.
  • Particularly preferred compounds D are water, diethyl ether, ethylamine, THF, n-propanol, formic acid, acetic acid, trifluoroacetic acid, trichloroacetic acid, sulfuric acid, phosphoric acid, trifluoromethanesulfonic acid and toluenesulfonic acid.
  • substituted used in the context of this application in connection with the various types of metathesis catalysts or compounds of the general formula (Z) means that a hydrogen atom on a specified radical or atom is replaced by one of the groups indicated in each case, with the proviso that the valence of the specified atom is not exceeded and the substitution leads to a stable compound.
  • the metathesis catalysts to be used in the process according to the invention are complex catalysts based on a metal of the 6th or 8th subgroup of the Periodic Table. These complex catalysts have the common structural feature of having at least one ligand carbene-like bound to the metal. In a preferred embodiment, the complex catalyst has two carbene ligands, ie two ligands which are carbene-like bound to the central metal of the complex. As metals of the 6th and 8th subgroup of the periodic table molybdenum, tungsten, osmium and ruthenium are preferred.
  • the one radical R is hydrogen and the other radical R is C 1 -C 20 -alkyl, C 3 -C 10 -cycloalkyl, C 2 -C 20 -alkenyl, C 2 -C 20- alkynyl, C 6 -C 24 -aryl, C 1 -C 20 -carboxylate, C 1 -C 20 -alkoxy, C 2 -C 20 -alkenyloxy, C 2 -C 20 -alkynyloxy, C 6 -C 24 - Aryloxy, C 2 -C 20 -alkoxycarbonyl, C 1 -C 30 -alkylamino, C 1 -C 30 -alkylthio, C 6 -C 24 -arylthio, C 1 -C 20 -alkylsulfonyl or C 1 -C 20 -alkylsulfinyl, these radicals may each be substituted by one
  • X 1 and X 2 are identical or different and represent two ligands, preferably anionic ligands.
  • X 1 and X 2 may, for example, be hydrogen, halogen, pseudohalogen, straight-chain or branched C 1 -C 30 -alkyl, C 6 -C 24 -aryl, C 1 -C 20 -alkoxy, C 6 -C 24 -aryloxy, C 3 -C 20 alkyl diketonate, C 6 -C 24 aryl diketonate, C 1 -C 20 carboxylate, C 1 -C 20 alkyl sulfonate, C 6 -C 24 aryl sulfonate, C 1 -C 20 alkylthiol, C 6 -C 24 -arylthiol, C 1 -C 20 -alkylsulfonyl or C 1 -C 20 -alkylsulfinyl radicals.
  • radicals X 1 and X 2 may be further substituted by one or more further radicals, for example by halogen, preferably fluorine, C 1 -C 10 alkyl, C 1 -C 10 -alkoxy or C 6 -C 24 aryl, these radicals may optionally in turn be substituted by one or more substituents selected from the group consisting of halogen, preferably fluorine, C 1 -C 5 alkyl, C 1 -C 5 alkoxy and phenyl.
  • halogen preferably fluorine, C 1 -C 10 alkyl, C 1 -C 10 -alkoxy or C 6 -C 24 aryl
  • substituents selected from the group consisting of halogen, preferably fluorine, C 1 -C 5 alkyl, C 1 -C 5 alkoxy and phenyl.
  • X 1 and X 2 are identical or different and are halogen, in particular fluorine, chlorine, bromine or iodine, benzoate, C 1 -C 5 -carboxylate, C 1 -C 5 -alkyl, phenoxy, C 1 -C 5 -alkoxy, C 1 -C 5 -alkylthiol, C 6 -C 24 -arylthiol, C 6 -C 24 -aryl or C 1 -C 5 -alkylsulfonate.
  • halogen in particular fluorine, chlorine, bromine or iodine
  • X 1 and X 2 are identical and are halogen, in particular chlorine, CF 3 COO, CH 3 COO, CFH 2 COO, (CH 3 ) 3 CO, (CF 3 ) 2 (CH 3 ) CO, ( CF 3 ) (CH 3 ) 2 CO, PhO (phenoxy), MeO (methoxy), EtO (ethoxy), tosylate (p-CH 3 -C 6 H 4 -SO 3 ), mesylate (2,4,6-trimethylphenyl ) or CF 3 SO 3 (trifluoromethanesulfonate).
  • L are the same or different ligands and preferably neutral electron donors.
  • the two ligands L for example, independently of each other, a phosphine, sulfonated phosphine, phosphate, phosphinite, phosphonite, arsine, stibin, ether, amine, amide, sulfoxide, carboxyl, nitrosyl, pyridine , Thioether or imidazolidine (“Im”) ligands.
  • the two ligands L independently of one another denote a C 6 -C 24 -aryl, C 1 -C 10 -alkyl or C 3 -C 20 -cycloalkyl-phosphine ligand, a sulfonated C 6 -C 24 -aryl or sulfonated C 1 -C 10 alkyl phosphine ligands, a C 6 -C 24 aryl or C 1 -C 10 alkyl phosphinite ligand, a C 6 -C 24 aryl or C 1 -C 10 Alkyl phosphonite ligands, a C 6 -C 24 aryl or C 1 -C 10 alkyl phosphite ligand, a C 6 -C 24 aryl or C 1 -C 10 alkylarsine ligand, a C 6 -C 24 -aryl or C 1 -C 10 -alkylamine ligands
  • phosphine includes, for example, PPh 3 , P (p-tolyl) 3 , P (o-tolyl) 3 , PPhenyl (CH 3 ) 2 , P (CF 3 ) 3 , P (p-FC 6 H 4 ) 3 , P (p-CF 3 C 6 H 4 ) 3 , P (C 6 H 4 -SO 3 Na) 3 , P (CH 2 C 6 H 4 -SO 3 Na) 3 , P (iso-propyl) 3 , P (CHCH 3 (CH 2 CH 3 )) 3 , P (cyclopentyl) 3 , P (cyclohexyl) 3 , P (neopentyl) 3 and P (neophenyl) 3 .
  • phosphinite includes, for example, triphenylphosphinite, tricyclohexylphosphinite, triisopropylphosphinite and methyldiphenylphosphinite.
  • phosphite includes, for example, triphenyl phosphite, tricyclohexyl phosphite, tri-tert-butyl phosphite, triisopropyl phosphite and methyl diphenyl phosphite.
  • stibin includes, for example, triphenylstibin, tricyclohexylstibin and trimethylstibene.
  • sulfonate includes, for example, trifluoromethanesulfonate, tosylate and mesylate.
  • thioether includes, for example, CH 3 SCH 3 , C 6 H 5 SCH 3 , CH 3 OCH 2 CH 2 SCH 3 and tetrahydrothiophene.
  • pyridine is intended to include in the context of this application as a generic term all nitrogen-containing ligands such as those in the WO-A-03/011455 be mentioned. Examples of these are: pyridine, picolines ( ⁇ -, ⁇ - and ⁇ -picoline), lutidines (2,3-, 2,4-, 2,5-, 2,6-, 3,4-and 3,5-lutidine), collidine (2,4,6-trimethylpyridine), trifluoromethylpyridine, phenylpyridine, 4- (dimethylamino) pyridine, chloropyridines, bromopyridines, nitropyridines, quinoline, pyrimidine, pyrrole, imidazole and phenylimidazole.
  • R 8 , R 9 , R 10 , R 11 may independently be substituted by one or more substituents, preferably straight or branched C 1 -C 10 alkyl, C 3 -C 8 cycloalkyl, C 1 -C 10 -alkoxy or C 6 -C 24 -aryl be substituted, these aforementioned substituents in turn by one or more radicals, preferably selected from the group halogen, in particular chlorine or bromine, C 1 -C 5 alkyl, C 1 -C 5 Alkoxy and phenyl may be substituted.
  • substituents preferably straight or branched C 1 -C 10 alkyl, C 3 -C 8 cycloalkyl, C 1 -C 10 -alkoxy or C 6 -C 24 -aryl be substituted, these aforementioned substituents in turn by one or more radicals, preferably selected from the group halogen, in particular chlorine or bromine, C 1 -C 5 alkyl, C 1 -C
  • R 8 and R 9 independently of one another are hydrogen, C 6 -C 24 -aryl, particularly preferably phenyl, straight-chain or branched C 1 -C 10 -alkyl, particularly preferably propyl or butyl or together form, together with the carbon atoms to which they are attached, a cycloalkyl or aryl radical, it being possible for all of the abovementioned radicals to be substituted by one or more further radicals selected from the group comprising straight-chain or branched C 1 - C 10 alkyl, C 1 -C 10 alkoxy, C 6 -C 24 aryl and a functional group selected from the group of hydroxy, thiol, thioether, ketone, aldehyde, ester, ether, amine, imine, amide, nitro , Carboxylic acid, disulfide, carbonate, isocyanate, carbodiimide, carboalk
  • the radicals R 10 and R 11 are identical or different and are straight-chain or branched C 1 -C 10 -alkyl, particularly preferably i-propyl or neopentyl, C 3 -C 10 -Cycloalkyl, preferably adamantyl, C 6 -C 24 -aryl, more preferably phenyl, C 1 -C 10 -alkyl sulfonate, more preferably methanesulfonate, C 6 -C 10 -arylsulfonate, more preferably p-toluenesulfonate.
  • radicals as meanings of R 10 and R 11 are substituted by one or more further radicals selected from the group comprising straight-chain or branched C 1 -C 5 -alkyl, in particular methyl, C 1 -C 5 -alkoxy, aryl and a functional group selected from the group of hydroxy, thiol, thioether, ketone, aldehyde, ester, ether, amine, imine, amide, nitro, carboxylic acid, disulfide, carbonate, isocyanate, carbodiimide, carboalkoxy, carbamate and halogen.
  • further radicals selected from the group comprising straight-chain or branched C 1 -C 5 -alkyl, in particular methyl, C 1 -C 5 -alkoxy, aryl and a functional group selected from the group of hydroxy, thiol, thioether, ketone, aldehyde, ester, ether, amine, imine, amide,
  • radicals R 10 and R 11 may be the same or different and are i-propyl, neopentyl, adamantyl, mesityl or 2,6-diisopropylphenyl.
  • imidazolidine radicals (Im) have the following structures (IIIa) to (IIIf), where Ph is in each case a phenyl radical, Bu is a butyl radical and Mes is 2,4,6-trimethylphenyl radical or Mes is alternative in all cases represents 2,6-diisopropylphenyl.
  • Various representatives of the catalysts of the formula (A) are known in principle, for example from the WO-A-96/04289 and the WO-A-97/06185 ,
  • one or both ligands L in the general formula (A) preferably also represents identical or different trialkylphosphine ligands, in which at least one of the alkyl groups represents a secondary alkyl group or a cycloalkyl group, preferably isopropyl, iso- Butyl, sec-butyl, neopentyl, cyclopentyl or cyclohexyl.
  • Particularly preferred in the general formula (A) is one or both ligands L for a trialkylphosphine ligand wherein at least one of the alkyl groups represents a secondary alkyl group or a cycloalkyl group, preferably iso-propyl, iso-butyl, sec-butyl, neo-pentyl, cyclopentyl or cyclohexyl.
  • catalyst systems which comprise, in addition to at least one compound of the general formula (Z), one of the following two catalysts which fall under the general formula (A) and the structures (IV) (Grubbs (I) catalyst) and (V) (Grubbs (II) catalyst) wherein Cy is cyclohexyl and Mes is mesityl.
  • This catalyst also referred to in the literature as "Nolan catalyst”, is for example made WO 2004/112951 known.
  • the catalysts of general formula (B) are known in principle. Representatives of this class of compounds are the catalysts described by Hoveyda et al. in US 2002/0107138 A1 and Angew. Chem. Int. Ed. 2003, 42, 4592 and the catalysts described by Grela in WO-A-2004/035596 . Eur. J. Org. Chem 2003, 963-966 and Angew. Chem. Int. Ed. 2002, 41, 4038 as in J. Org. Chem. 2004, 69, 6894-96 and Chem. Eur. J 2004, 10, 777-784 to be discribed. The catalysts are commercially available or can be prepared according to the cited references.
  • L is a ligand which usually has an electron-donor function and can assume the same general, preferred and particularly preferred meanings as L in the general formula (A).
  • L in the general formula (B) is preferably a P (R 7 ) 3 radical, where R 7 is independently C 1 -C 6 alkyl, C 3 -C 8 cycloalkyl or aryl, or optionally substituted imidazolidine residue ("Im").
  • C 1 -C 6 -alkyl is, for example, methyl, ethyl, n-propyl, isopropyl, n-butyl, sec-butyl, tert-butyl, n-pentyl, 1-methylbutyl, 2-methylbutyl, 3 Methylbutyl, neo-pentyl, 1-ethylpropyl and n-hexyl.
  • C 3 -C 8 cycloalkyl includes cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl and cyclooctyl.
  • Aryl comprises an aromatic radical having 6 to 24 skeletal carbon atoms.
  • Preferred mono-, bi- or tricyclic carbocyclic aromatic radicals having 6 to 10 skeletal carbon atoms are, for example, phenyl, biphenyl, naphthyl, phenanthrenyl or anthracenyl.
  • R 8 , R 9 , R 10 , R 11 may independently be substituted by one or more substituents, preferably straight or branched C 1 -C 10 alkyl, C 3 -C 8 cycloalkyl, C 1 -C 10 -alkoxy or C 6 -C 24 -aryl be substituted, these aforementioned substituents in turn by one or more radicals, preferably selected from the group halogen, in particular chlorine or bromine, C 1 -C 5 alkyl, C 1 -C 5 Alkoxy and phenyl may be substituted.
  • substituents preferably straight or branched C 1 -C 10 alkyl, C 3 -C 8 cycloalkyl, C 1 -C 10 -alkoxy or C 6 -C 24 -aryl be substituted, these aforementioned substituents in turn by one or more radicals, preferably selected from the group halogen, in particular chlorine or bromine, C 1 -C 5 alkyl, C 1 -C
  • catalysts of the general formula (B) in which R 8 and R 9 independently of one another are hydrogen, C 6 -C 24 -aryl, are particularly preferred Phenyl, straight-chain or branched C 1 -C 10 -alkyl, particularly preferably propyl or butyl, or together form, including the carbon atoms to which they are attached, a cycloalkyl or aryl radical, all of the abovementioned radicals optionally in turn being replaced by a or a plurality of further radicals selected from the group comprising straight-chain or branched C 1 -C 10 -alkyl, C 1 -C 10 -alkoxy, C 6 -C 24 -aryl and a functional group selected from the group of hydroxyl, Thiol, thioether, ketone, aldehyde, ester, ether, amine, imine, amide,
  • radicals as meanings of R 10 and R 11 are substituted by one or more further radicals selected from the group comprising straight-chain or branched C 1 -C 5 -alkyl, in particular methyl, C 1 -C 5 -alkoxy, aryl and a functional group selected from the group of hydroxy, thiol, thioether, ketone, aldehyde, ester, ether, amine, Imine, amide, nitro, carboxylic acid, disulfide, carbonate, isocyanate, carbodiimide, carboalkoxy, carbamate and halogen.
  • further radicals selected from the group comprising straight-chain or branched C 1 -C 5 -alkyl, in particular methyl, C 1 -C 5 -alkoxy, aryl and a functional group selected from the group of hydroxy, thiol, thioether, ketone, aldehyde, ester, ether, amine, Imine, amide,
  • radicals R 10 and R 11 may be identical or different and denote i-propyl, neopentyl, adamantyl or mesityl.
  • imidazolidine radicals (Im) have the previously mentioned structures (IIIa-IIIf), wherein each Mes is 2,4,6-trimethylphenyl.
  • X 1 and X 2 are identical or different and may be, for example, hydrogen, halogen, pseudohalogen, straight-chain or branched C 1 -C 30 alkyl, C 6 -C 24 -aryl, C 1 -C 20 -alkoxy, C 6 -C 24 -aryloxy, C 3 -C 20 -alkyl diketonate, C 6 -C 24 -aryl diketonate, C 1 -C 20 -carboxylate, C 1 -C 20 -alkyl sulfonate, C 6 -C 24 - Arylsulfonate, C 1 -C 20 -alkylthiol, C 6 -C 24 -arylthiol, C 1 -C 20 -alkylsulfonyl or C 1 -C 20 -alkylsulfinyl.
  • radicals X 1 and X 2 may be further substituted by one or more further radicals, for example by halogen, preferably fluorine, C 1 -C 10 alkyl, C 1 -C 10 -alkoxy or C 6 -C 24 -aryl radicals, wherein the latter radicals may optionally in turn be substituted by one or more substituents selected from the group consisting of halogen, preferably fluorine, C 1 -C 5 alkyl, C 1 -C 5 alkoxy and phenyl.
  • halogen preferably fluorine, C 1 -C 10 alkyl, C 1 -C 10 -alkoxy or C 6 -C 24 -aryl radicals
  • substituents selected from the group consisting of halogen, preferably fluorine, C 1 -C 5 alkyl, C 1 -C 5 alkoxy and phenyl.
  • X 1 and X 2 are identical or different and are halogen, in particular fluorine, chlorine, bromine or iodine, benzoate, C 1 -C 5 -carboxylate, C 1 -C 5 -alkyl, phenoxy, C 1 -C 5 -alkoxy, C 1 -C 5 -alkylthiol, C 6 -C 24 -arylthiol, C 6 -C 24 -aryl or C 1 -C 5 -alkylsulfonate.
  • halogen in particular fluorine, chlorine, bromine or iodine
  • X 1 and X 2 are identical and are halogen, in particular chlorine, CF 3 COO, CH 3 COO, CFH 2 COO, (CH 3 ) 3 CO, (CF 3 ) 2 (CH 3 ) CO, ( CF 3 ) (CH 3 ) 2 CO, PhO (phenoxy), MeO (methoxy), EtO (ethoxy), tosylate (p-CH 3 -C 6 H 4 -SO 3 ), mesylate (2,4,6-trimethylphenyl ) or CF 3 SO 3 (trifluoromethanesulfonate).
  • the radical R 1 is an alkyl, cycloalkyl, alkenyl, alkynyl, aryl, alkoxy, alkenyloxy, alkinyloxy, aryloxy, alkoxycarbonyl, alkylamino, alkylthio, arylthio -, Alkylsulfonyl- or alkylsulfinyl radical, each of which may be in each case optionally substituted by one or more alkyl, halogen, alkoxy, aryl or heteroaryl radicals.
  • the radical R 1 usually denotes a C 1 -C 30 -alkyl, C 3 -C 20 -cycloalkyl, C 2 -C 20 -alkenyl, C 2 -C 20 -alkynyl, C 6 -C 24 -aryl, C 1 - C 20 alkoxy, C 2 -C 20 alkenyloxy, C 2 -C 20 alkynyloxy, C 6 -C 24 aryloxy, C 2 -C 20 alkoxycarbonyl, C 1 -C 20 alkylamino, C 1 -C 20 -alkylthio, C 6 -C 24 -arylthio, C 1 -C 20 -alkylsulfonyl or C 1 -C 20 -alkylsulfinyl radical, all of which are each optionally substituted by one or more alkyl, halogen, alkoxy, aryl or heteroaryl Radicals may be substituted.
  • R 1 is a C 3 -C 20 -cycloalkyl radical, a C 6 -C 24 -aryl radical or a straight-chain or branched C 1 -C 30 -alkyl radical, the latter being optionally substituted by one or more double or triple bonds or one or more heteroatoms, preferably oxygen or nitrogen, may be interrupted.
  • R 1 is a straight-chain or branched C 1 -C 12 -alkyl radical.
  • the C 3 -C 20 cycloalkyl radical includes, for example, cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl and cyclooctyl.
  • the C 1 -C 12 -alkyl radical may be, for example, methyl, ethyl, n-propyl, isopropyl, n-butyl, sec-butyl, tert-butyl, n-pentyl, 1-methylbutyl, 2-methylbutyl, 3-methylbutyl, neo-pentyl, 1-ethylpropyl, n-hexyl, n-heptyl, n-octyl, n-decyl or n-dodecyl.
  • R 1 is methyl or isopropyl.
  • the C 6 -C 24 aryl radical represents an aromatic radical having 6 to 24 skeleton carbon atoms.
  • Preferred mono-, bi- or tricyclic carbocyclic aromatic radicals having 6 to 10 skeletal carbon atoms are, for example, phenyl, biphenyl, naphthyl, phenanthrenyl or anthracenyl.
  • radicals R 2 , R 3 , R 4 and R 5 are identical or different and may be hydrogen, organic or inorganic radicals.
  • R 2 , R 3 , R 4 , R 5 are identical or different and denote hydrogen, halogen, nitro, CF 3 , alkyl, cycloalkyl, alkenyl, alkynyl, aryl, alkoxy, alkenyloxy , Alkynyloxy, aryloxy, alkoxycarbonyl, alkylamino, alkylthio, arylthio, alkylsulfonyl or alkylsulfinyl radicals, all of which are each optionally substituted by one or more alkyl, alkoxy, halogen, aryl or heteroaryl radicals could be.
  • R 2 , R 3 , R 4 , R 5 are the same or different and are hydrogen, halogen, preferably chlorine or bromine, nitro, CF 3 , C 1 -C 30 alkyl, C 3 -C 20 -cycloalkyl, C 2 -C 20 alkenyl, C 2 -C 20 alkynyl, C 6 -C 24 -aryl, C 1 -C 20 -alkoxy, C 2 -C 20 -alkenyloxy, C 2 -C 20 -alkynyloxy, C 6 -C 24 -aryloxy, C 2 -C 20 -alkoxycarbonyl, C 1 -C 20 alkylamino, C 1 -C 20 alkylthio, C 6 -C 24 arylthio, C 1 -C 20 alkylsulfonyl or C 1 -C 20 alkylsulfinyl radicals, all of which are each optionally substituted by one or more C 1
  • R 2 , R 3 , R 4 , R 5 are identical or different and are nitro, straight-chain or branched C 1 -C 30 -alkyl, C 5 -C 20 -cycloalkyl, straight-chain or branched C 1 -C 20 -alkoxy radicals or C 6 -C 24 -aryl radicals, preferably phenyl or naphthyl.
  • the C 1 -C 30 -alkyl radicals and C 1 -C 20 -alkoxy radicals may optionally be interrupted by one or more double or triple bonds or else one or more heteroatoms, preferably oxygen or nitrogen.
  • R 2 , R 3 , R 4 or R 5 may also be bridged via aliphatic or aromatic structures.
  • R 3 and R 4 can form a fused-on phenyl ring including the carbon atoms to which they are bonded in the phenyl ring of formula (B) to result in a total naphthyl structure.
  • the radical R 6 is hydrogen, an alkyl, alkenyl, alkynyl or an aryl radical.
  • R 6 is preferably hydrogen, a C 1 -C 30 -alkyl, a C 2 -C 20 -alkenyl, a C 2 -C 20 -alkynyl or a C 6 -C 24 -aryl radical. More preferably R 6 is hydrogen.
  • the catalysts of general formula (B1) are, for example US 2002/0107138 A1 (Hoveyda et al. ) in principle known and can be obtained according to the manufacturing process specified there.
  • a catalyst system comprising at least one compound of the general formula (Z) and a catalyst which falls under the general structural formula (B1) and has the formula (VII) where Mes is in each case 2,4,6-trimethylphenyl stands.
  • This catalyst (VII) is also referred to in the literature as "Hoveyda catalyst”.
  • catalyst systems are those which, in addition to at least one compound of the general formula (Z), comprise a catalyst which falls under the general structural formula (B1) and has one of the following formulas (VIII), (IX), (X), ( XI), (XII), (XIII), (XIV) and (XV), wherein each Mes is 2,4,6-trimethylphenyl.
  • the catalysts of general formula (B2) are for example WO-A-2004/035596 (Grela) in principle known and can be obtained according to the manufacturing process specified there.
  • the catalyst (XVI) is also referred to in the literature as a "Grela catalyst".
  • Another suitable catalyst system comprises at least one compound of the general formula (Z) and a catalyst which falls under the general formula (B2) and has the following structure (XVII), wherein each Mes is 2,4,6-trimethylphenyl.
  • the catalysts according to the general formula (B3) are made US 2002/0107138 A1 known and produced according to the information given there.
  • a further alternative embodiment relates to the use of a catalyst system comprising at least one compound of the general formula (Z) and a catalyst of the formula (B4), where the symbol stands for a carrier.
  • the support is preferably a poly (styrenedivinylbenzene) copolymer (PS-DVB).
  • PS-DVB poly (styrenedivinylbenzene) copolymer
  • the catalysts according to formula (B4) are made Chem. Eur. J. 2004 10, 777-784 known in principle and available according to the preparation methods described therein.
  • All of the aforementioned catalysts of type (B) can either be used as such in the reaction mixture of the NBR metathesis or else be applied to a solid support and immobilized.
  • Suitable solid phases or carriers are those materials which, on the one hand, are inert to the metathesis reaction mixture and, on the other hand, do not impair the activity of the catalyst.
  • immobilization of the catalyst it is possible to use, for example, metals, glass, polymers, ceramics, organic polymer beads or also inorganic sol gels, carbon black, silica, silicates, calcium carbonate and barium sulfate.
  • the catalysts of general formula (C) are known in principle (see, for example Angew. Chem. Int. Ed. 2004, 43, 6161-6165 ).
  • X 1 and X 2 in the general formula (C) may have the same general, preferred and particularly preferred meanings as in the formulas (A) and (B).
  • the imidazolidine residue (Im) usually has a structure of the general formulas (IIa) or (IIb) which have already been mentioned for the catalyst type of the formulas (A) and (B) and may also have all the structures mentioned there as preferred, in particular having the formulas (IIIa) - (IIIf).
  • the radicals R 'in the general formula (C) are identical or different and denote a straight-chain or branched C 1 -C 30 alkyl, C 5 -C 30 -cycloalkyl or aryl radical, where the C 1 -C 30 - Alkyl radicals may optionally be interrupted by one or more double or triple bonds or one or more heteroatoms, preferably oxygen or nitrogen.
  • Aryl comprises an aromatic radical having 6 to 24 skeletal carbon atoms.
  • Preferred mono-, bi- or tricyclic carbocyclic aromatic radicals having 6 to 10 skeletal carbon atoms are, for example, phenyl, biphenyl, naphthyl, phenanthrenyl or anthracenyl.
  • radicals R 'in the general formula (C) are preferably identical and are phenyl, cyclohexyl, cyclopentyl, isopropyl, o-tolyl, o-xylyl or mesityl.
  • the catalysts of the general formulas (G), (H) and (K) are known in principle, for example from WO 2003/011455 A1 . WO 2003/087167 A2 . Organometallics 2001, 20, 5314 and Angew. Chem. Int. Ed. 2002, 41, 4038 , The catalysts are commercially available or can be synthesized by the production methods indicated in the abovementioned references.
  • Catalysts of the general formulas (G), (H) and (K) in which Z 1 and Z 2 are identical or different and represent neutral electron donors are used in the catalyst systems which can be used according to the invention.
  • These ligands are usually weakly coordinating. Typically, these are optionally substituted heterocyclic groups.
  • These may be five or six-membered monocyclic groups having from 1 to 4, preferably 1 to 3, and more preferably 1 or 2 heteroatoms or two or polycyclic structures of 2, 3, 4 or 5 such five or six membered monocyclic groups, all in each case above-mentioned groups optionally by one or more alkyl, preferably C 1 -C 10 -alkyl, cycloalkyl, preferably C 3 -C 8 -cycloalkyl, alkoxy, preferably C 1 -C 10 -alkoxy, halogen, preferably chlorine or bromine, aryl, preferably C 6 -C 24 -aryl, or heteroaryl, preferably C 5 -C 23 heteroaryl radicals, each again by one or more groups, preferably selected from the group consisting of halogen, in particular chlorine or bromine, C 1 -C 5 Alkyl, C 1 -C 5 alkoxy and phenyl.
  • alkyl preferably C 1 -C 10 -alkyl,
  • Z 1 and Z 2 include nitrogen-containing heterocycles such as pyridines, pyridazines, bipyridines, pyrimidines, pyrazines, pyrazolidines, pyrrolidines, piperazines, indazoles, quinolines, purines, acridines, bisimidazoles, picolylimines, imidazolidines and pyrroles.
  • nitrogen-containing heterocycles such as pyridines, pyridazines, bipyridines, pyrimidines, pyrazines, pyrazolidines, pyrrolidines, piperazines, indazoles, quinolines, purines, acridines, bisimidazoles, picolylimines, imidazolidines and pyrroles.
  • Z 1 and Z 2 may also be bridged together to form a cyclic structure.
  • Z 1 and Z 2 are a single bidentate ligand.
  • R 21 and R 22 are identical or different and are alkyl, preferably C 1 -C 30 -alkyl, more preferably C 1 -C 20 -alkyl, cycloalkyl preferably C 3 -C 20 -cycloalkyl, particularly preferably C 3 -C 8 -cycloalkyl, alkenyl, preferably C 2 -C 20 -alkenyl, particularly preferably C 2 -C 16 -alkenyl, alkynyl, preferably C 2 -C 20 - alkynyl, more preferably C 2 -C 16 alkynyl, aryl, preferably, C 6 -C 24 -aryl, carboxylate, preferably C 1 -C 20 -carboxylate, alkoxy, preferably C 1 -C 20 -alkoxy, alkenyloxy, preferably C 2 C 20 -alkenyloxy, alkynyl
  • X 1 and X 2 are the same or different and may have the same general, preferred and particularly preferred meanings as previously for X 1 and X 2 in the general formula (A) indicated.
  • Halogen radicals preferably fluorine, chlorine or bromine, C 1 -C 5 alkyl, C 1 -C 5 alkoxy or phenyl
  • catalyst of the formula (XIX) have the structures (XIX a) or (XIX b), wherein R 23 and R 24 have the same meanings as indicated in the formula (XIX).
  • the catalysts to be used according to the invention in the catalyst systems have the structural element of the general formula (N1), where the carbon atom marked with a " * " is bound to the catalyst skeleton via one or more double bonds. If the carbon atom marked with a " * " is bound to the catalyst skeleton via two or more double bonds, these double bonds can be cumulated or conjugated.
  • the structural element of the general formula (N1) is bonded via conjugated double bonds to the metal of the complex catalyst. In both cases, there is a double bond in the direction of the central metal of the complex catalyst at the C atom marked with a " * ".
  • the catalysts of the general formula (N2a) and (N2b) thus comprise catalysts in which the following general structural elements (N3) - (N9) via the C atom characterized by a " * " via one or more double bonds to the catalyst skeleton of the general formula (N10a) or (N10b) wherein X 1 and X 2 , L 1 and L 2 , n, n 'and R 25 -R 39 have the meanings given for the general formulas (N2a) and (N2b).
  • the ruthenium or osmium carbene catalysts of the invention are five-coordinate.
  • C 1 -C 6 -alkyl in the structural element of the general formula (N 1 ) is , for example, methyl, ethyl, n-propyl, isopropyl, n-butyl, sec-butyl, tert-butyl, n-pentyl, Methylbutyl, 2-methylbutyl, 3-methylbutyl, neo-pentyl, 1-ethylpropyl and n-hexyl.
  • C 3 -C 8 -cycloalkyl in the structural element of the general formula (N1) is , for example, cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl and cyclooctyl.
  • C 6 -C 24 -aryl comprises an aromatic radical having 6 to 24 skeletal carbon atoms .
  • Preferred mono-, bi- or tricyclic carbocyclic aromatic radicals having 6 to 10 skeletal carbon atoms are, for example, phenyl, biphenyl, naphthyl, phenanthrenyl or anthracenyl.
  • radicals X 1 and X 2 in the structural element of the general formula (N1) have the same general, preferred and particularly preferred meanings that are mentioned for catalysts of the general formula A.
  • radicals L 1 and L 2 are identical or different ligands, preferably neutral electron donors, and may have the same general, have preferred and particularly preferred meanings which are mentioned for the catalysts of general formula A.
  • the compounds of the general formula (N1-azo) are 9-diazofluorene or various derivatives thereof, depending on the meaning of the radicals R 25 -R 32 and A.
  • a wide variety of derivatives of 9-diazo-fluorene can be used. In this way, a wide variety of Fluorenylidenderivate are accessible.
  • the catalyst precursor compounds are ruthenium or osmium complex catalysts which do not yet contain a ligand having the general structural element (N1).
  • Suitable for carrying out the reaction are saturated, unsaturated and aromatic hydrocarbons, ethers and halogenated solvents. Preference is given to chlorinated solvents such as dichloromethane, 1,2-dichloroethane or chlorobenzene.
  • the catalyst precursor compound is introduced in the form of the ruthenium or osmium precursor in a preferably dried solvent.
  • the concentration of the ruthenium or osmium precursor in the solvent is usually in the range of 15 to 25% by weight, preferably in the range of 15 to 20% by weight.
  • the solution can be heated. It has proven particularly useful to heat to a temperature in the range of 30 to 50 ° C.
  • the compound of the general formula (N1-azo) dissolved in usually dried, preferably anhydrous solvent is added.
  • concentration of the compound of general formula (N1-azo) in the solvent is preferably in the range of 5 to 15% by weight, preferably about 10%.
  • the temperature is particularly preferably in the same range as mentioned above, ie at 30 to 50 ° C.
  • the solvent is removed and the residue is purified by extraction, for example with a mixture of hexane with an aromatic solvent.
  • the catalyst according to the invention is not obtained in the pure form but in an equimolar mixture due to the stoichiometry of the reaction with the reaction product of the compound of the general formula (N1-azo) with the leaving ligand of the catalyst precursor compound used in the reaction.
  • the leaving ligand is a phosphine ligand.
  • This reaction product can be removed to obtain the pure catalyst of the invention.
  • the pure catalyst according to the invention can be used, but also the mixture of this catalyst according to the invention with the aforementioned reaction product.
  • the compound of general formula (Z) can be added in a solvent or dispersant or else without solvent or dispersant to the complex catalyst or its solution, thereby System to receive.
  • Preferred dispersants include, but are not limited to, acetone, benzene, chlorobenzene, chloroform, cyclohexane, dichloromethane, diethyl ether, dioxane, dimethylformamide, dimethylacetamide, dimethylsulfone, dimethylsulfoxide, methyl ethyl ketone, tetrahydrofuran, tetrahydropyran, and toluene.
  • the solvent or dispersant is inert to the complex catalyst.
  • the aforementioned catalyst systems are used according to the invention for the metathesis of nitrile rubber.
  • the use according to the invention is then a process for reducing the molecular weight of the nitrile rubber by bringing the nitrile rubber into contact with the catalyst system according to the invention. This reaction represents a cross metathesis.
  • the compound of the general formula (Z) can be added to a solution of the complex catalyst in a solvent or dispersant or even without a solvent or dispersant.
  • the compound of general formula (Z) can also be added directly to a solution of the nitrile rubber to be degraded, to which moreover the complex catalyst is added so that the entire catalyst system according to the invention is present in the reaction mixture.
  • the amount of the complex catalyst based on the nitrile rubber used depends on the nature and catalytic activity of the specific complex catalyst.
  • the amount of complex catalyst used is usually 1 to 1000 ppm noble metal, preferably 2 to 500 ppm, in particular 5 to 250 ppm, based on the nitrile rubber used.
  • the NBR metathesis can be carried out in the absence or in the presence of a co-olefin.
  • this co-olefin is preferably a straight-chain or branched C 2 -C 16 olefin. Suitable examples are ethylene, propylene, isobutene, styrene, 1-hexene or 1-octene. Preference is given to using 1-hexene or 1-octene.
  • the co-olefin is liquid (such as, for example, 1-hexene)
  • the amount of the co-olefin is preferably in a range of 0.2-20% by weight, based on the nitrile rubber used.
  • the amount of co-olefin is chosen so that a pressure in the range of 1 x 10 5 Pa - 1 x 10 7 Pa is established in the reaction vessel at room temperature, preferably a pressure in the range of 5.2 x 10 5 Pa to 4 x 10 6 Pa.
  • the metathesis reaction can be carried out in a suitable solvent which does not deactivate the catalyst used and also does not adversely affect the reaction in any other way.
  • suitable solvents include, but are not limited to, dichloromethane, benzene, toluene, methyl ethyl ketone, acetone, tetrahydrofuran, tetrahydropyran, dioxane, cyclohexane and chlorobenzene.
  • the most preferred solvent is chlorobenzene.
  • when the co-olefin itself can act as a solvent e.g. with 1-hexene, can be dispensed with the addition of a further additional solvent.
  • the concentration of the nitrile rubber used in the metathesis reaction mixture is not critical, but it should of course be noted that the reaction should not be adversely affected by too high a viscosity of the reaction mixture and the associated mixing problems.
  • the concentration of NBR in the reaction mixture is preferably in the range from 1 to 25% by weight, more preferably in the range from 5 to 20% by weight, based on the total reaction mixture.
  • the metathesis degradation is usually carried out at a temperature in the range of 10 ° C to 150 ° C, preferably at a temperature in the range of 20 to 100 ° C.
  • the reaction time depends on a number of factors, for example the type of NBR, the type of catalyst, the catalyst concentration used and the reaction temperature. Typically, the reaction is complete within five hours under normal conditions.
  • the progress of the metathesis can be monitored by standard analysis, e.g. by GPC measurements or by determining the viscosity.
  • NBR nitrile rubbers
  • NBR nitrile rubbers
  • the conjugated diene can be of any nature. Preference is given to using (C 4 -C 6 ) conjugated dienes. Particular preference is given to 1,3-butadiene, isoprene, 2,3-dimethylbutadiene, piperylene or mixtures thereof. Particular preference is given to 1,3-butadiene and isoprene or mixtures thereof. Very particular preference is given to 1,3-butadiene.
  • any known ⁇ , ⁇ -unsaturated nitrile can be used, preferred are (C 3 -C 5 ) - ⁇ , ⁇ -unsaturated nitriles such as acrylonitrile, methacrylonitrile, ethacrylonitrile or mixtures thereof. Particularly preferred is acrylonitrile.
  • a particularly preferred nitrile rubber thus represents a copolymer of acrylonitrile and 1,3-butadiene.
  • one or more further copolymerizable monomers known to those skilled in the art may also be used, e.g. ⁇ , ⁇ -unsaturated mono- or dicarboxylic acids, their esters or amides. Fumaric acid, maleic acid, acrylic acid and methacrylic acid are preferred as ⁇ , ⁇ -unsaturated mono- or dicarboxylic acids.
  • esters of the ⁇ , ⁇ -unsaturated carboxylic acids their alkyl esters and alkoxyalkyl esters are preferably used.
  • alkyl esters of the ⁇ , ⁇ -unsaturated carboxylic acids are methyl acrylate, ethyl acrylate, butyl acrylate, butyl methacrylate, 2-ethylhexyl acrylate, 2-ethylhexyl methacrylate and octyl acrylate.
  • Particularly preferred alkoxyalkyl esters of the ⁇ , ⁇ -unsaturated carboxylic acids are methoxyethyl (meth) acrylate, ethoxyethyl (meth) acrylate and methoxyethyl (meth) acrylate. It is also possible to use mixtures of alkyl esters, such as e.g. the foregoing, with alkoxyalkyl esters, e.g. in the form of the aforementioned.
  • the proportions of conjugated diene and ⁇ , ⁇ -unsaturated nitrile in the NBR polymers to be used can vary widely.
  • the proportion of or the sum of the conjugated dienes is usually in the range of 40 to 90 wt .-%, preferably in the range of 60 to 85 wt.%, Based on the total polymer.
  • the proportion of or the sum of ⁇ , ⁇ -unsaturated Nitriles are usually from 10 to 60% by weight, preferably from 15 to 40% by weight, based on the total polymer.
  • the proportions of the monomers in each case add up to 100% by weight.
  • the additional monomers can be present in amounts of from 0 to 40% by weight, preferably from 0.1 to 40% by weight, particularly preferably from 1 to 30% by weight, based on the total polymer.
  • corresponding proportions of the conjugated dienes and / or of the ⁇ , ⁇ -unsaturated nitriles are replaced by the proportions of the additional monomers, the proportions of all monomers adding up to 100% by weight in each case.
  • Nitrile rubbers which can be used in the inventive mind are also commercially available, eg as products from the product range of the brands Perbuna ® and Krynac ® from Lanxess Germany GmbH.
  • the nitrile rubbers used for the metathesis have a Mooney viscosity (ML 1 + 4 at 100 ° C) in the range of 30 to 70, preferably from 30 to 50. This corresponds to a weight average molecular weight M w in the range of 150,000 - 500,000, preferably in Range of 180,000-400,000.
  • the Mooney viscosity is determined according to ASTM standard D 1646.
  • the nitrile rubbers obtained by the metathesis process of the present invention have a Mooney viscosity (ML 1 + 4 at 100 ° C) in the range of 5 to 30, preferably in the range of 5 to 20. This corresponds to a weight average molecular weight M w in the range of 10,000-100,000, preferably in the range of 10,000-80,000.
  • Hydrogenation of the resulting degraded nitrile rubbers can follow the metathesis degradation in the presence of the catalyst system according to the invention. This can be done in a manner known to those skilled in the art.
  • the catalysts used are usually based on rhodium, ruthenium or titanium, but it is also possible to use platinum, iridium, palladium, rhenium, ruthenium, osmium, cobalt or copper either as metal or preferably in the form of metal compounds (see, for example, US Pat US-A-3,700,637 . DE-A-25 39 132 . EP-A-0 134 023 . DE-OS 35 41 689 . DE-OS 35 40 918 . EP-A-0 298 386 . DE-OS 35 29 252 . DE-OS 34 33 392 . US-A-4,464,515 and US-A-4,503,196 ).
  • Suitable catalysts and solvents for homogeneous phase hydrogenation are described below and are also exhaustive DE-A-25 39 132 and the EP-A-0 471 250 known.
  • Preferred catalysts are tris (triphenylphosphine) rhodium (I) chloride, tris (triphenylphosphine) rhodium (III) chloride and tris (dimethyl sulfoxide) rhodium (III) chloride and tetrakis ( triphenylphosphine) rhodium hydride of the formula (C 6 H 5 ) 3 P) 4 RhH and the corresponding compounds in which the triphenylphosphine has been wholly or partly replaced by tricyclohexylphosphine.
  • the catalyst can be used in small quantities. An amount in the range of 0.01-1% by weight, preferably in the range of 0.03-0.5% by weight, and more preferably in the range of 0.1-0.3% by weight based on the weight of the polymer are suitable.
  • co-catalyst which is a ligand of the formula R 1 m B, where R 1 , m and B have the meanings given above for the catalyst.
  • R 1 , m and B have the meanings given above for the catalyst.
  • m is 3
  • B is phosphorus and the radicals R 1 may be the same or different.
  • co-catalysts with trialkyl, tricycloalkyl, triaryl, triaralkyl, diaryl-monoalkyl, diaryl-monocycloalkyl, dialkyl-monoaryl, dialkylmonocycloalkyl, dicycloalkyl-monoaryl or dicyclalkyl-monoaryl radicals.
  • co-catalysts can be found, for example, in US-A-4,631,315 , Preferred co-catalyst is triphenylphosphine.
  • the co-catalyst is preferably used in amounts within a range of 0.1-5 wt.%, Preferably in the range of 0.3-4 wt.%, Based on the weight of the nitrile rubber to be hydrogenated.
  • the weight ratio of the rhodium-containing catalyst to the co-catalyst is preferably in the range from 1: 3 to 1:55, particularly preferably in the range from 1: 5 to 1:45.
  • the co-catalyst Based on 100 parts by weight of the nitrile rubber to be hydrogenated, suitably 0.1 to 33 parts by weight of the co-catalyst, preferably 0.5 to 20 and most preferably 1 to 5 parts by weight, especially more than 2 but less than 5 parts by weight of co-catalyst based 100 parts by weight of the nitrile rubber to be hydrogenated.
  • hydrogenation is understood as meaning a conversion of the double bonds present in the starting nitrile rubber to at least 50%, preferably 70-100%, particularly preferably 80-100%. Residue contents of double bonds in the HNBR of 0 to 8% are also particularly preferred.
  • heterogeneous catalysts are usually supported catalysts based on palladium, z. B. supported on carbon, silica, calcium carbonate or barium sulfate.
  • a hydrogenated nitrile rubber having a Mooney Viscosity (ML 1 + 4 @ 100 ° C), measured according to ASTM Standard D 1646, in the range 1-50 is obtained.
  • Mooney Viscosity (ML 1 + 4 @ 100 ° C) is in the range of 5 to 30.
  • Mooney viscosity (ML 1 + 4 @ 100 ° C) is in the range of 5 to 30. This corresponds approximately to a weight average molecular weight M w in the range of about 20,000 - 200,000.
  • the catalyst system is not only successfully used for the metathesis degradation of nitrile rubbers, but also universally for other metathesis reactions.
  • the catalyst system according to the invention with the corresponding acyclic starting material, such as diethyl diallylmalonate in contact.
  • the amount of the actual metathesis catalyst and thus the amount of noble metal can be significantly reduced with respect to analogous metathesis reactions at comparable reaction times only the catalyst; ie without the addition of a fluorine-containing boron compound of the general formula (Z) is used.
  • the reaction time is substantially shortened by the addition of the fluorine-containing boron compound of the general formula (Z).
  • degraded nitrile rubbers with significantly lower molecular weights M w and M n can be achieved.
  • This nitrile rubber had the following characteristics: acrylonitrile content: 34.3% by weight Mooney Viscosity (ML 1 + 4 @ 100 ° C): 33 Mooney units Residual moisture: 1.0% by weight M w : 211 kg / mol M n: 82 kg / mol PDI (M w / M n ): 2.6
  • the Ru catalysts (Grubbs II, Hoveyda and Grela catalyst) were each dissolved in 10 g of inertized MCB under argon, with the addition of the catalyst solutions to the NBR solutions in MCB being carried out immediately after preparation of the catalyst solutions.
  • the solutions were each filtered by means of a 0.2 ⁇ m syringe filter made of Teflon (Chromafil PTFE 0.2 mm, Machery-Nagel). Subsequently, the GPC analysis was carried out with a device from Waters (mod. 510). For the analysis, a combination of a precolumn (PL Guard from Polymer Laboratories) with two Resipore columns (300x7.5 mm, pore size 3 microns) from Polymer Laboratories was used. The calibration of the columns was carried out using linear polystyrene of molecular weights from 960 to 6 x 10 5 g / mol from Polymer Standards Services.
  • PL Guard from Polymer Laboratories
  • Resipore columns 300x7.5 mm, pore size 3 microns
  • the detector used was a Waters RI detector (Waters 410 Differential Refractometer). The analysis was carried out at a flow rate of 1.0 mL / min at 80 ° C using N, N'-dimethylacetamide as the eluent. The evaluation of the GPC curves was carried out with software from Polymer Laboratories (Cirrus Multi Version 3.0)
  • Test series 1 Use of the Grubbs II catalyst in combination with various fluorine-containing boron compounds in the metathesis degradation of NBR
  • Test series 2 Use of the Grela catalyst in combination with BF 3 * Et 2 O in the metathesis degradation of NBR

Landscapes

  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Catalysts (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
EP09164639A 2008-07-08 2009-07-06 Méthode pour la réduction du poid moléculaire de caoutchouc nitrilé Not-in-force EP2145681B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP09164639A EP2145681B1 (fr) 2008-07-08 2009-07-06 Méthode pour la réduction du poid moléculaire de caoutchouc nitrilé

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP08159917A EP2147721A1 (fr) 2008-07-08 2008-07-08 Systèmes des catalyseurs et usage en réactions de métathèse
EP09164639A EP2145681B1 (fr) 2008-07-08 2009-07-06 Méthode pour la réduction du poid moléculaire de caoutchouc nitrilé

Publications (2)

Publication Number Publication Date
EP2145681A1 true EP2145681A1 (fr) 2010-01-20
EP2145681B1 EP2145681B1 (fr) 2013-02-27

Family

ID=39720260

Family Applications (2)

Application Number Title Priority Date Filing Date
EP08159917A Withdrawn EP2147721A1 (fr) 2008-07-08 2008-07-08 Systèmes des catalyseurs et usage en réactions de métathèse
EP09164639A Not-in-force EP2145681B1 (fr) 2008-07-08 2009-07-06 Méthode pour la réduction du poid moléculaire de caoutchouc nitrilé

Family Applications Before (1)

Application Number Title Priority Date Filing Date
EP08159917A Withdrawn EP2147721A1 (fr) 2008-07-08 2008-07-08 Systèmes des catalyseurs et usage en réactions de métathèse

Country Status (6)

Country Link
US (1) US8536277B2 (fr)
EP (2) EP2147721A1 (fr)
JP (1) JP5564208B2 (fr)
CN (1) CN101624428B (fr)
BR (1) BRPI0904864A2 (fr)
CA (1) CA2670380A1 (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2418225A1 (fr) 2010-08-09 2012-02-15 LANXESS Deutschland GmbH Caoutchoucs nitriles partiellement hydrogénés
EP2484700A1 (fr) 2011-02-04 2012-08-08 LANXESS Deutschland GmbH Caoutchoucs nitriles fonctionnalisés et leur fabrication
US9598506B2 (en) 2011-10-21 2017-03-21 Arlanxeo Deutschland Gmbh Catalyst compositions and their use for hydrogenation of nitrile rubber
WO2020120207A3 (fr) * 2018-12-12 2020-08-20 Arlanxeo Deutschland Gmbh Système catalyseur contenant un catalyseur de métathèse et au moins un composé phénolique et procédé de métathèse de caoutchouc nitrile-butadiène (nbr) à l'aide du système catalyseur

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2289623A1 (fr) * 2009-08-31 2011-03-02 LANXESS Deutschland GmbH Métathèse de caoutchoucs de nitrile en présence de catalyseurs de métal de transition
WO2013056461A1 (fr) 2011-10-21 2013-04-25 Lanxess Deutschland Gmbh Compositions catalytiques et leur utilisation pour l'hydrogénation d'un caoutchouc de nitrile
WO2013056400A1 (fr) * 2011-10-21 2013-04-25 Lanxess Deutschland Gmbh Compositions catalytiques et leur utilisation pour l'hydrogénation d'un caoutchouc de nitrile
WO2013056463A1 (fr) 2011-10-21 2013-04-25 Lanxess Deutschland Gmbh Compositions catalytiques et leur utilisation pour l'hydrogénation de caoutchouc nitrile
DE102014105885A1 (de) * 2014-04-25 2015-10-29 Universität Stuttgart N-Heterozyklische Carbenkomplexe von Metallimidoalkylidenen und Metalloxoalkylidenen und deren Verwendung
TWI566835B (zh) 2014-12-25 2017-01-21 財團法人工業技術研究院 烯烴複分解觸媒及低分子量丁腈橡膠之製備方法
PL3353187T3 (pl) 2015-09-24 2021-11-22 Umicore Ag & Co. Kg Katalizatory metatezy olefin na bazie karbenu metalu
US10465031B2 (en) 2015-11-06 2019-11-05 Hydril USA Distribution LLC Short-chain fluorocarbon-grafted elastomer blowout preventer packers and seals for enhanced H2S resistance
CN107556489B (zh) * 2017-10-16 2020-06-19 山东理工大学 一种压力控制的自旋交叉分子磁性材料及其制备方法
KR102702569B1 (ko) 2017-12-08 2024-09-06 아란세오 도이치란드 게엠베하 루테늄 착물 촉매를 사용하여 니트릴 고무를 생성하기 위한 방법
EP3827030B1 (fr) 2018-07-23 2024-03-27 ARLANXEO Deutschland GmbH Hydrogénation de caoutchouc nitrile
US11414587B2 (en) * 2020-05-22 2022-08-16 Halliburton Energy Services, Inc. Cycloalkene and transition metal compound catalyst resin for well sealing

Citations (30)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3700637A (en) 1970-05-08 1972-10-24 Shell Oil Co Diene-nitrile rubbers
DE2539132A1 (de) 1975-09-03 1977-03-17 Bayer Ag Hydrierung von polymeren
US4464515A (en) 1982-12-08 1984-08-07 Polysar Limited Polymer hydrogenation process
US4503196A (en) 1982-12-08 1985-03-05 Polysar Limited Polymer hydrogenation process
EP0134023A1 (fr) 1983-08-19 1985-03-13 Bayer Ag Préparation de caoutchouc nitrile hydrogéné
DE3433392A1 (de) 1984-09-12 1986-03-20 Bayer Ag, 5090 Leverkusen Hydrierung nitrilgruppenhaltiger ungesaettigter polymerer
DE3529252A1 (de) 1985-08-16 1987-02-19 Bayer Ag Verfahren zur selektiven hydrierung ungesaettigter verbindungen
DE3540918A1 (de) 1985-11-19 1987-05-21 Bayer Ag Verfahren zur selektiven hydrierung ungesaettigter verbindungen
DE3541689A1 (de) 1985-11-26 1987-05-27 Bayer Ag Verfahren zur selektiven hydrierung nitrilgruppenhaltiger ungesaettigter polymerer
EP0298386A2 (fr) 1987-07-06 1989-01-11 University Of Waterloo Procédé d'hydrogénation de polymères
EP0419952A1 (fr) 1989-09-26 1991-04-03 Bayer Ag Procédé de préparation de caoutchouc nitrile hydrogéné à viscosité modérée
EP0471250A1 (fr) 1990-08-15 1992-02-19 Bayer Ag Copolymères de butadiène/isoprène/(méth)acrylonitrile hydrogénés
WO1996004289A1 (fr) 1992-04-03 1996-02-15 California Institute Of Technology Complexes carbeniques de ruthenium et d'osmium a haute activite pour reactions de metathese des olefines, et leur procede de synthese
WO1997006185A1 (fr) 1995-08-03 1997-02-20 California Institute Of Technology Complexes carbene - ruthenium/osmium, activant fortement les reactions de metathese
WO2000071554A2 (fr) 1999-05-24 2000-11-30 California Institute Of Technology Catalyseurs de metathese de carbene metallique a base d'imidazolidine
US20020107138A1 (en) 2000-08-10 2002-08-08 Hoveyda Amir H. Recyclable metathesis catalysts
WO2002100941A1 (fr) 2001-06-12 2002-12-19 Bayer Inc. Caoutchouc nitrile hydrogene de faible poids moleculaire
WO2002100905A1 (fr) 2001-06-12 2002-12-19 Bayer Inc. Procede de preparation de caoutchouc nitrile hydrogene de faible poids moleculaire
WO2003002613A1 (fr) 2001-06-29 2003-01-09 Bayer Inc. Caoutchouc nitrile ayant un faible poids moleculaire
WO2003011455A1 (fr) 2001-08-01 2003-02-13 California Institute Of Technology Catalyseurs de metathese de carbene metallique de ruthenium ou d'osmium hexacoordonnes
WO2003087167A2 (fr) 2002-04-05 2003-10-23 California Institute Of Technology Metathese croisee d'olefines directement substituees par un groupe accepteur d'electrons a l'aide de catalyseurs au carbene de metaux de transition
US6683136B2 (en) 2000-12-28 2004-01-27 Bayer Inc. Epoxidized soybean oil enhanced hydrogenation of nitrile copolymer
WO2004035679A1 (fr) * 2002-10-17 2004-04-29 Bayer Inc. Melanges polymeres comprenant une plasticite de nitrile a faible poids moleculaire
WO2004035596A1 (fr) 2002-10-15 2004-04-29 Boehringer Ingelheim International Gmbh Complexes de ruthenium en tant que (pre)catalyseurs de reaction de metathese
US20040095792A1 (en) * 1998-04-06 2004-05-20 Herrmann Wolfgang Anton Alkylidene complexes of ruthenium containing N-heterocyclic carbene ligands; use as highly active, selective catalysts for olefin metathesis
US20040132891A1 (en) 2002-12-05 2004-07-08 Ong Christopher M. Process for the preparation of low molecular weight hydrogenated nitrile rubber
WO2004112951A2 (fr) 2003-06-19 2004-12-29 University Of New Orleans Research & Technology Foundation, Inc. Preparation de catalyseurs a base de ruthenium pour la metathese d'olefines
EP1825913A1 (fr) 2006-02-22 2007-08-29 Lanxess Deutschland GmbH & Co.KG Nouveau système de catalyseur et son utilisation pour des réactions de métathèse
EP1894946A2 (fr) 2006-08-30 2008-03-05 Lanxess Deutschland GmbH Procédé de décomposition de caoutchouc nitrile par métathèse
DE102007039695A1 (de) 2007-08-22 2009-02-26 Lanxess Deutschland Gmbh Katalysatoren für Metathese-Reaktionen

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4812528A (en) * 1987-07-06 1989-03-14 University Of Waterloo Polymer hydrogenation process
US5143992A (en) * 1991-07-12 1992-09-01 Shell Oil Company Methathesis polymerizable adducts of a divinylcyclohydrocarbon and cyclopentadiene
US5405924A (en) * 1993-07-22 1995-04-11 Shell Oil Company Imido transition metal complex metathesis catalysts
DE19902439A1 (de) * 1999-01-22 2000-08-03 Aventis Res & Tech Gmbh & Co Homo- und heterobimetallische Alkylidenkomplexe des Rutheniums mit N-heterocyclischen Carbenliganden und deren Anwendung als hochaktive, selektive Katalysatoren für die Olefin-Metathese
US7329758B1 (en) * 1999-05-24 2008-02-12 California Institute Of Technology Imidazolidine-based metal carbene metathesis catalysts
US6759537B2 (en) * 2001-03-23 2004-07-06 California Institute Of Technology Hexacoordinated ruthenium or osmium metal carbene metathesis catalysts
CA2462005A1 (fr) * 2004-02-23 2005-08-23 Bayer Inc. Methode de preparation de caoutchouc nitrile hydrogene de bas poids moleculaire
EP2027920B1 (fr) * 2007-08-21 2014-10-08 LANXESS Deutschland GmbH Catalyseurs pour les réactions de metathèses
CN101205242A (zh) * 2007-09-30 2008-06-25 埃沃尼克德古萨有限责任公司 含有n-杂环卡宾配体的钌的亚烷基络合物及其在烯烃复分解反应中作为高活性高选择性催化剂的用途
US20110206882A1 (en) 2010-02-24 2011-08-25 Norman Scott Broyles Injection stretch blow molding process

Patent Citations (32)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3700637A (en) 1970-05-08 1972-10-24 Shell Oil Co Diene-nitrile rubbers
DE2539132A1 (de) 1975-09-03 1977-03-17 Bayer Ag Hydrierung von polymeren
US4464515A (en) 1982-12-08 1984-08-07 Polysar Limited Polymer hydrogenation process
US4503196A (en) 1982-12-08 1985-03-05 Polysar Limited Polymer hydrogenation process
EP0134023A1 (fr) 1983-08-19 1985-03-13 Bayer Ag Préparation de caoutchouc nitrile hydrogéné
DE3433392A1 (de) 1984-09-12 1986-03-20 Bayer Ag, 5090 Leverkusen Hydrierung nitrilgruppenhaltiger ungesaettigter polymerer
US4631315A (en) 1984-09-12 1986-12-23 Bayer Aktiengesellschaft Hydrogenation of nitrile group-containing unsaturated polymers
DE3529252A1 (de) 1985-08-16 1987-02-19 Bayer Ag Verfahren zur selektiven hydrierung ungesaettigter verbindungen
DE3540918A1 (de) 1985-11-19 1987-05-21 Bayer Ag Verfahren zur selektiven hydrierung ungesaettigter verbindungen
DE3541689A1 (de) 1985-11-26 1987-05-27 Bayer Ag Verfahren zur selektiven hydrierung nitrilgruppenhaltiger ungesaettigter polymerer
EP0298386A2 (fr) 1987-07-06 1989-01-11 University Of Waterloo Procédé d'hydrogénation de polymères
EP0419952A1 (fr) 1989-09-26 1991-04-03 Bayer Ag Procédé de préparation de caoutchouc nitrile hydrogéné à viscosité modérée
EP0471250A1 (fr) 1990-08-15 1992-02-19 Bayer Ag Copolymères de butadiène/isoprène/(méth)acrylonitrile hydrogénés
WO1996004289A1 (fr) 1992-04-03 1996-02-15 California Institute Of Technology Complexes carbeniques de ruthenium et d'osmium a haute activite pour reactions de metathese des olefines, et leur procede de synthese
WO1997006185A1 (fr) 1995-08-03 1997-02-20 California Institute Of Technology Complexes carbene - ruthenium/osmium, activant fortement les reactions de metathese
US20040095792A1 (en) * 1998-04-06 2004-05-20 Herrmann Wolfgang Anton Alkylidene complexes of ruthenium containing N-heterocyclic carbene ligands; use as highly active, selective catalysts for olefin metathesis
WO2000071554A2 (fr) 1999-05-24 2000-11-30 California Institute Of Technology Catalyseurs de metathese de carbene metallique a base d'imidazolidine
US20020107138A1 (en) 2000-08-10 2002-08-08 Hoveyda Amir H. Recyclable metathesis catalysts
US6683136B2 (en) 2000-12-28 2004-01-27 Bayer Inc. Epoxidized soybean oil enhanced hydrogenation of nitrile copolymer
WO2002100905A1 (fr) 2001-06-12 2002-12-19 Bayer Inc. Procede de preparation de caoutchouc nitrile hydrogene de faible poids moleculaire
WO2002100941A1 (fr) 2001-06-12 2002-12-19 Bayer Inc. Caoutchouc nitrile hydrogene de faible poids moleculaire
WO2003002613A1 (fr) 2001-06-29 2003-01-09 Bayer Inc. Caoutchouc nitrile ayant un faible poids moleculaire
WO2003011455A1 (fr) 2001-08-01 2003-02-13 California Institute Of Technology Catalyseurs de metathese de carbene metallique de ruthenium ou d'osmium hexacoordonnes
WO2003087167A2 (fr) 2002-04-05 2003-10-23 California Institute Of Technology Metathese croisee d'olefines directement substituees par un groupe accepteur d'electrons a l'aide de catalyseurs au carbene de metaux de transition
WO2004035596A1 (fr) 2002-10-15 2004-04-29 Boehringer Ingelheim International Gmbh Complexes de ruthenium en tant que (pre)catalyseurs de reaction de metathese
WO2004035679A1 (fr) * 2002-10-17 2004-04-29 Bayer Inc. Melanges polymeres comprenant une plasticite de nitrile a faible poids moleculaire
US20040127647A1 (en) 2002-10-17 2004-07-01 Ong Christopher M. Polymer blends comprising low molecular weight nitrile rubber
US20040132891A1 (en) 2002-12-05 2004-07-08 Ong Christopher M. Process for the preparation of low molecular weight hydrogenated nitrile rubber
WO2004112951A2 (fr) 2003-06-19 2004-12-29 University Of New Orleans Research & Technology Foundation, Inc. Preparation de catalyseurs a base de ruthenium pour la metathese d'olefines
EP1825913A1 (fr) 2006-02-22 2007-08-29 Lanxess Deutschland GmbH & Co.KG Nouveau système de catalyseur et son utilisation pour des réactions de métathèse
EP1894946A2 (fr) 2006-08-30 2008-03-05 Lanxess Deutschland GmbH Procédé de décomposition de caoutchouc nitrile par métathèse
DE102007039695A1 (de) 2007-08-22 2009-02-26 Lanxess Deutschland Gmbh Katalysatoren für Metathese-Reaktionen

Non-Patent Citations (22)

* Cited by examiner, † Cited by third party
Title
ANGEW. CHEM. INT. ED. 2002, vol. 41, pages 4038
ANGEW. CHEM. INT. ED., vol. 41, 2002, pages 4038
ANGEW. CHEM. INT. ED., vol. 42, 2003, pages 4592
ANGEW. CHEM. INT. ED., vol. 43, 2004, pages 6161 - 6165
CHEM. EUR. J, vol. 10, 2004, pages 777 - 784
CHEM. EUR. J., vol. 10, 2004, pages 777 - 784
DER EINSATZ DES IN INORGANICA CHIMICA ACTA, vol. 359, 2006, pages 2910 - 2917
EUR. J. ORG. CHEM, 2003, pages 963 - 966
FURSTNER, ALOIS ET AL: "Cationic ruthenium allenylidene complexes as catalysts for ring closing olefin metathesis", CHEMISTRY--A EUROPEAN JOURNAL ( 2000 ), 6(10), 1847-1857 CODEN: CEUJED; ISSN: 0947-6539, 2000, XP002494975 *
FUSTERO, SANTOS ET AL: "Microwave-Assisted Tandem Cross Metathesis Intramolecular Aza-Michael Reaction: An Easy Entry to Cyclic .beta.-Amino Carbonyl Derivatives", JOURNAL OF THE AMERICAN CHEMICAL SOCIETY ( 2007 ), 129(21), 6700-6701 CODEN: JACSAT; ISSN: 0002-7863, 2007, XP002494974 *
INORGANICA CHIMICA ACTA, vol. 359, 2006, pages 2910 - 2917
J. ORG. CHEM., vol. 68, 2003, pages 2020 - 2023
J. ORG. CHEM., vol. 69, 2004, pages 6894 - 96
J.AM.CHEM. SOC., vol. 119, 1997, pages 3887 - 3897
J.AM.CHEM.SOC., vol. 119, 1997, pages 3887 - 3897
J.AM.CHEM.SOC., vol. 119, 1997, pages 9130 - 9136
KELSEY, DONALD R. ET AL: "In situ catalyst systems for ring-opening metathesis polymerization", JOURNAL OF POLYMER SCIENCE, PART A: POLYMER CHEMISTRY , 35(14), 3027-3047 CODEN: JPACEC; ISSN: 0887-624X, 1997, XP002494976 *
LEDOUX ET AL: "In situ generation of highly active olefin metathesis initiators", JOURNAL OF ORGANOMETALLIC CHEMISTRY, ELSEVIER-SEQUOIA S.A. LAUSANNE, CH, vol. 691, no. 24-25, 24 November 2006 (2006-11-24), pages 5482 - 5486, XP025188912, ISSN: 0022-328X *
ORG. BIOMOL. CHEM., vol. 3, no. 4, 2005, pages 139 - 4142
ORGANOMETALLICS, vol. 20, 2001, pages 5314
PLATINUM METALS REV., vol. 49, no. 3, 2005, pages 123 - 137
SYNLETT, no. 4, 2005, pages 670 - 672

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2418225A1 (fr) 2010-08-09 2012-02-15 LANXESS Deutschland GmbH Caoutchoucs nitriles partiellement hydrogénés
WO2012019978A1 (fr) 2010-08-09 2012-02-16 Lanxess Deutschland Gmbh Caoutchoucs nitriles partiellement hydrogénés
EP2484700A1 (fr) 2011-02-04 2012-08-08 LANXESS Deutschland GmbH Caoutchoucs nitriles fonctionnalisés et leur fabrication
WO2012104183A1 (fr) 2011-02-04 2012-08-09 Lanxess Deutschland Gmbh Caoutchoucs nitriles fonctionnalisés et fabrication desdits caoutchoucs nitriles
US10011664B2 (en) 2011-02-04 2018-07-03 Arlanxeo Deutschland Gmbh Functionalized nitrile rubbers and the production thereof
US9598506B2 (en) 2011-10-21 2017-03-21 Arlanxeo Deutschland Gmbh Catalyst compositions and their use for hydrogenation of nitrile rubber
WO2020120207A3 (fr) * 2018-12-12 2020-08-20 Arlanxeo Deutschland Gmbh Système catalyseur contenant un catalyseur de métathèse et au moins un composé phénolique et procédé de métathèse de caoutchouc nitrile-butadiène (nbr) à l'aide du système catalyseur
US11673130B2 (en) 2018-12-12 2023-06-13 Arlanxeo Deutschland Gmbh Catalyst system containing a metathesis catalyst and at least one phenolic compound and a process for metathesis of nitrile-butadiene rubber (NBR) using the catalyst system

Also Published As

Publication number Publication date
US8536277B2 (en) 2013-09-17
JP5564208B2 (ja) 2014-07-30
BRPI0904864A2 (pt) 2013-07-02
CA2670380A1 (fr) 2010-01-08
US20100087600A1 (en) 2010-04-08
JP2010018801A (ja) 2010-01-28
CN101624428A (zh) 2010-01-13
CN101624428B (zh) 2013-08-28
EP2145681B1 (fr) 2013-02-27
EP2147721A1 (fr) 2010-01-27

Similar Documents

Publication Publication Date Title
EP2145681B1 (fr) Méthode pour la réduction du poid moléculaire de caoutchouc nitrilé
EP2027919B1 (fr) Système de catalyseur comprenant un chlorure d'un metal alcalinoterreux et son utilisation pour les réactions de métathèse
EP2143489A1 (fr) Systèmes de catalyseurs et usage en réactions de métathèse
EP2030988B1 (fr) Procédé de décomposition par métathèse de caoutchouc nitrile
EP1894946B1 (fr) Procédé de décomposition de caoutchouc nitrile par métathèse
EP2027920B1 (fr) Catalyseurs pour les réactions de metathèses
EP1826220B1 (fr) Utilisation de catalyseurs à activité accrue pour la métathèse de caoutchoucs nitriles
EP1825913B1 (fr) Nouveau système de catalyseur et son utilisation pour des réactions de métathèse
EP1760093B1 (fr) Utilisation de catalyseurs pour la dégradation de caoutchouc nitrile par métathèse
DE60219011T3 (de) Hydrierter nitrilkautschuk mit niedrigem molekulargewicht
EP2484700B1 (fr) Caoutchoucs nitriles fonctionnalisés et leur fabrication
JP2009046681A (ja) 遷移金属錯体触媒存在下におけるニトリルゴムのメタセシス
EP2603533B1 (fr) Caoutchoucs nitriles partiellement hydrogénés
DE102007039527A1 (de) Katalysatoren für Metathese-Reaktionen
EP3720885B1 (fr) Procédé de fabrication de caoutchouc de nitrile au moyen des catalyseurs complexes de ruthénium
DE102005040939A1 (de) Neuer Katalysator für den Metatheseabbau von Nitrilkautschuk
DE102005058834A1 (de) Neuer Katalysator für den Metatheseabbau von Nitrilkautschuk
DE102007039695A1 (de) Katalysatoren für Metathese-Reaktionen
DE102005048327A1 (de) Neuer Katalysator für den Metatheseabbau von Nitrilkautschuk

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK SM TR

AX Request for extension of the european patent

Extension state: AL BA RS

17P Request for examination filed

Effective date: 20100720

17Q First examination report despatched

Effective date: 20100817

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK SM TR

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

Free format text: NOT ENGLISH

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: AT

Ref legal event code: REF

Ref document number: 598200

Country of ref document: AT

Kind code of ref document: T

Effective date: 20130315

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

Free format text: LANGUAGE OF EP DOCUMENT: GERMAN

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 502009006352

Country of ref document: DE

Effective date: 20130425

REG Reference to a national code

Ref country code: LT

Ref legal event code: MG4D

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130527

Ref country code: SE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130227

Ref country code: ES

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130607

Ref country code: LT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130227

Ref country code: IS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130627

Ref country code: BG

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130527

REG Reference to a national code

Ref country code: NL

Ref legal event code: VDEP

Effective date: 20130227

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130227

Ref country code: PL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130227

Ref country code: PT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130627

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130227

Ref country code: LV

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130227

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130528

RAP2 Party data changed (patent owner data changed or rights of a patent transferred)

Owner name: LANXESS DEUTSCHLAND GMBH

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: HR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130227

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CZ

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130227

Ref country code: RO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130227

Ref country code: DK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130227

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130227

Ref country code: EE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130227

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130227

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CY

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130227

REG Reference to a national code

Ref country code: DE

Ref legal event code: R081

Ref document number: 502009006352

Country of ref document: DE

Owner name: LANXESS DEUTSCHLAND GMBH, DE

Free format text: FORMER OWNER: LANXESS DEUTSCHLAND GMBH, 51373 LEVERKUSEN, DE

Effective date: 20131113

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

BERE Be: lapsed

Owner name: LANXESS DEUTSCHLAND G.M.B.H.

Effective date: 20130731

26N No opposition filed

Effective date: 20131128

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MC

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130227

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 502009006352

Country of ref document: DE

Effective date: 20131128

REG Reference to a national code

Ref country code: IE

Ref legal event code: MM4A

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20130731

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20130731

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20130731

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20130706

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20140702

Year of fee payment: 6

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20140708

Year of fee payment: 6

Ref country code: GB

Payment date: 20140702

Year of fee payment: 6

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: IT

Payment date: 20140718

Year of fee payment: 6

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SM

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130227

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130227

Ref country code: TR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130227

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20130706

Ref country code: HU

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO

Effective date: 20090706

Ref country code: MK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130227

REG Reference to a national code

Ref country code: AT

Ref legal event code: MM01

Ref document number: 598200

Country of ref document: AT

Kind code of ref document: T

Effective date: 20140706

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20140706

REG Reference to a national code

Ref country code: DE

Ref legal event code: R119

Ref document number: 502009006352

Country of ref document: DE

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20150706

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20160202

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20150706

Ref country code: IT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20150706

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

Effective date: 20160331

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20150731